Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L45/00—Compositions of homopolymers or copolymers of compounds having no unsaturated aliphatic radicals in side chain, and having one or more carbon-to-carbon double bonds in a carbocyclic or in a heterocyclic ring system; Compositions of derivatives of such polymers
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K3/00—Use of inorganic substances as compounding ingredients
  • C08K3/02—Elements
  • C08K3/04—Carbon
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K3/00—Use of inorganic substances as compounding ingredients
  • C08K3/34—Silicon-containing compounds
  • C08K3/36—Silica
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L15/00—Compositions of rubber derivatives
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
  • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L23/04—Homopolymers or copolymers of ethene
  • C08L23/08—Copolymers of ethene
  • C08L23/0807—Copolymers of ethene with unsaturated hydrocarbons only containing more than three carbon atoms
  • C08L23/0815—Copolymers of ethene with aliphatic 1-olefins
  • C08L23/0823—Copolymers of ethene with aliphatic cyclic olefins
• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
  • C09K3/00—Materials not provided for elsewhere
  • C09K3/10—Materials in mouldable or extrudable form for sealing or packing joints or covers

Definitions

• the present disclosure relates to a rubber composition and a method for reducing adhesion to the surface of a kneading machine using the same. More particularly, the present disclosure relates to an ethylene/butene/5-ethylidene-2-norbornene terpolymer rubber composition and a method for reducing adhesion to the surface of a kneading machine using the same.
• EPDM ethylene/propylene/diene copolymer rubber
• carbon black used in this rubber composition is not particularly limited, and that known carbon black, such as FEF carbon black and SRF carbon black, can be used. In each Example, it is merely described that carbon black is simply used.
• Patent Document 2 which discloses an ethylene/butene/non-conjugated polyene copolymer, indicates that various types of carbon black are used as reinforcing agents in a rubber composition comprising this copolymer.
• Asahi #55G GPF
• Asahi #50HG Grade
• Asahi #60G FEF
• Seast FEF FEF
• EBENB has a very high polymer copolymer adhesion. Due to adhesion to the surface of a kneading machine, particularly an open roll kneading machine, the productivity is extremely low in the rubber composition kneading process. In addition, there are problems, such as safety risk due to the intrusion of the operator's hand or arm into dangerous areas near the bank during reverse operation, and a concern for contamination of foreign matter etc.
• Patent Document 1 WO 2017/170190 A1
• Patent Document 2 JP-A-2011-213822
• An object of the present disclosure is to provide an ethylene/butene/5-ethylidene-2-norbornene terpolymer rubber composition to which carbon black having specific properties is added, the rubber composition being intended to reduce adhesion to the surface of a kneading machine in consideration of kneading processability.
• the above object of the present disclosure can be achieved by a rubber composition having a reduced adhesion to the surface of a kneading machine, the rubber composition comprising 20 to 60 parts by weight of carbon black having a DBP oil absorption of 100 ml/100 g or more and an iodine value of 75 to 90 g/kg based on 100 parts by weight of an ethylene/butene/5-ethylidene-2-norbornene terpolymer.
• the rubber composition of the present disclosure can effectively reduce adhesion to the surface of a kneading machine, particularly an open roll kneading machine, by compounding carbon black having specific properties. Further, stable and safe productivity can be obtained.
• This rubber composition is used as a seal parts, for which a high pressure gas sealing function is particularly required in a low temperature environment, e.g., about ⁇ 30 to ⁇ 60° C.
• the characteristics of rubber materials greatly affect the material costs of the entire rubber composition and the production efficiency.
• EBENB is superior in cold resistance as compounded with EPDM; therefore, a rubber composition having desired low temperature rubber characteristics can be achieved with a less compounding amount than EPDM, and the material costs can be reduced as the entire rubber composition.
• EBENB is more flexible as compounded with EPDM, is thus excellent in processability, such as kneadability, dispersibility and moldability, and greatly improves the production efficiency. Therefore, the costs in the production process can be reduced.
• the production costs of rubber molded products can be reduced, as compared with conventional rubber compositions using EPDM, in terms of the material costs and production efficiency.
• EBENB any one obtained by copolymerizing ethylene and butene with a small amount (about 0.1 to 20 wt. %, preferably about 3 to 15 wt. %) of 5-ethylidene-2-norbornene component can be used.
• commercial products such as Metallocene EBT (produced by Mitsui Chemicals, Inc.), can be used as they are.
• the iodine value of EBENB is preferably about 3 to 20 g/100 g, more preferably about 5 to 18 g/100 g. Within the above range, it is possible to prevent deterioration of rubber molded products due to excellent heat aging resistance and weather resistance, and to maintain a stable molecular state even in a low temperature environment, thereby improving low temperature sealing properties.
• EBENB has a lower polymer viscosity represented by Mooney viscosity ML 1+4 (100° C.) and superior processability (e.g., kneadability and moldability), as compared with EPDM. Therefore, the use of EBENB in place of EPDM improves productivity, such as molding efficiency, consequently reducing the production costs.
• the Mooney viscosity ML 1+4 (100° C.) of EBENB is preferably about 10 to 45, more preferably about 15 to 35. If the Mooney viscosity is too low, the compression set may increase, and the tensile strength may decrease. In contrast, if the Mooney viscosity is too high, the characteristics may be improved, but the processability may be deteriorated.
• the Mooney viscosity ML 1+4 (100° C.) can be determined according to the definition of JIS K 6300-1: 2013.
• the content of the ethylene component in EBENB is preferably about 60 to 80 wt. %, and more preferably about 65 to 75 wt. %. Within this range, the glass transition temperature Tg of EBENB shows the minimum value, and the cold resistance is improved.
• EBENB and EPDM can be used in combination, as long as the objects of the present disclosure are not impaired.
• hardness modifiers such as silicic acid, calcium carbonate, magnesium carbonate, clay, talc, bentonite, sericite, mica, calcium silicate, alumina hydrate, and barium sulfate
• resin-based fillers such as polyethylene, polypropylene, polystyrene, coumarone-indene resin, melamine resin, and phenol resin, can also be used in combination, if necessary.
• carbon black As carbon black [CB], one having a DBP oil absorption of 100 ml/100 g or more and an iodine value of 75 to 90, preferably 80 to 85 g/kg, is used.
• This is mainly HAF type carbon black; however, HAF-LS-SC (S-315) and HAF-LS (N-326) are not included because their DBP oil absorption is equal to or less than the specified value, although they are of HAF type.
• the DBP oil absorption is equal to or lower than this range, adhesion to the surface of the target kneading machine cannot be reduced at all. Further, if the iodine value is equal to or lower than this range, the effect of reducing adhesion to the surface of the kneading machine is not sufficient. In contrast, if the iodine value is equal to or greater than this range, the dispersibility of the filler is not sufficient, in addition to the insufficient adhesion reducing effect.
• Carbon black having such properties is used at a ratio of about 20 to 60 parts by weight based on 100 parts by weight of EBENB. If the compounding ratio is less than this range, the effect of reducing adhesion is not sufficiently exhibited. In contrast, if the compounding ratio is greater than this range, the rubber may not be wound, particularly when using an open roll kneading machine.
• carbon black having a DBP oil absorption of 100 ml/100 g or more and an iodine value of 30 to 130 g/kg, excluding 75 to 90 g/kg can be used in combination at a ratio of 50 parts by weight or less based on 100 parts by weight of EBENB.
• the total amount of both types of carbon black is preferably about 20 to 80 parts by weight.
• silica can be used as a filler in combination at a ratio of about 50 parts by weight or less based on 100 parts by weight of EBENB.
• silica it is preferable to use various silane coupling agents.
• the total amount of carbon black having specific properties and silica is preferably about 20 to 100 parts by weight.
• the crosslinking agent is mainly preferably an organic peroxide.
• organic peroxides include tert-butyl peroxide, dicumyl peroxide, 2,5-dimethyl-2,5-di-tert-butylperoxyhexane, 2,5-dimethyl-2,5-di-tert-butylperoxyhexine-3, tert-butylcumyl peroxide, 1,3-ditert-butylperoxyisopropylbenzene, 2,5-dimethyl-2,5-dibenzoylperoxyhexane, tert-butyl peroxybenzoate, tert-butyl peroxyisopropyl carbonate, n-butyl-4,4-di-tert-butylperoxyvalerate, and the like.
• the amount of crosslinking agent to be compounded is preferably about 0.5 to 10 parts by weight, more preferably about 1 to 5 parts by weight, based on 100 parts by weight of EBENB. Within the above range, it is possible to prevent that molding cannot be performed due to foaming during vulcanization. Further, since the crosslinking density becomes good, the resulting product is likely to have sufficient physical properties.
• a master batch containing the above-mentioned organic peroxide can also be used.
• Such a masterbatch is preferable from the viewpoint that kneadability and dispersibility can be improved during preparation of the rubber composition.
• a crosslinking accelerator may be contained, if necessary.
• the crosslinking accelerator triallyl isocyanurate, triallyl cyanate, liquid polybutadiene, N,N′-m-phenylenedimaleimide, trimethylolpropane trimethacrylate, or the like can be used.
• crosslinking efficiency can be improved, and further heat resistance and mechanical properties can be improved; thus, the stability as a seal part can also be improved.
• the rubber composition preferably further contains a processing aid and a lubricant.
• processing aid plasticizer
• process oils containing aliphatic hydrocarbon as a main component such as PW380 and PW220 (produced by Idemitsu Kosan Co., Ltd.). These can be used singly or in combination.
• process oils have a lower molecular weight as compared with paraffin wax having a similar chemical structure, and are thus more preferable from the viewpoint that they have a unique effect that cannot be achieved when paraffin wax is compounded.
• lubricant for example, Diamid O-200 and Diamid L-200 (produced by Nippon Kasei Chemical Company Limited), which are fatty acid amides, are used.
• the amounts of the processing aid and the lubricant to be compounded are each preferably about 1 to 20 parts by weight, more preferably about 3 to 15 parts by weight, based on 100 parts by weight of EBENB. Within the above range, kneading processability is improved, and the occurrence of oil bleeding can be prevented.
• the rubber composition may suitably contain, if necessary, compounding agents generally used in the rubber industry, such as plasticizer, acid acceptors, and antioxidants, as rubber compounding agents.
• compounding agents generally used in the rubber industry, such as plasticizer, acid acceptors, and antioxidants, as rubber compounding agents.
• the amount of rubber compounding agent to be compounded is preferably about 300 parts by weight or less based on 100 parts by weight of EBENB.
• the rubber composition can be prepared by kneading the various materials using a kneading machine, such as a single screw extruder, a twin screw extruder, a roll, a Banbury mixer, a kneader, or a high shear mixer.
• a kneading machine such as a single screw extruder, a twin screw extruder, a roll, a Banbury mixer, a kneader, or a high shear mixer.
• the rubber composition can be crosslinked by pressure vulcanization generally at about 150 to 230° C. for about 0.5 to 30 minutes using an injection molding machine, a compression molding machine, or the like.
• a secondary vulcanization may be performed, if necessary, in order to reliably vulcanize the inside of the vulcanized product.
• the secondary vulcanization can be generally performed by oven heating at about 150 to 250° C. for about 0.5 to 24 hours.
• the rubber molded product obtained by crosslinking and molding the rubber composition according to the present disclosure has excellent low temperature rubber characteristics particularly at ⁇ 50° C. and is suitable as a rubber molded product to be used in a low temperature environment (e.g., about ⁇ 40° C. to ⁇ 60° C.).
• a rubber molded product preferably has a TR10 value of ⁇ 50° C. or lower, as measured by the low temperature elastic recovery test specified in JIS K6261: 2006.
• the rubber molded product of the present disclosure preferably has an appropriate hardness.
• the Type A durometer hardness specified in JIS K6253-1: 2012 corresponding to ISO 18517 is preferably 65 to 95.
• the obtained rubber molded product examples include seal parts used for sealing high pressure gas of low temperature, insulators, vibration isolators, sound insulators, and the like.
• the rubber molded product is suitably used as a seal part used in a low temperature environment and having excellent low temperature sealing properties, particularly as a seal part for high pressure gas (e.g., high pressure hydrogen) equipment.
• high pressure gas e.g., high pressure hydrogen
• the shape of the rubber molded product according to the present disclosure is not particularly limited, and can be various shapes according to its application.
• Examples of the shape as the seal part include O-rings, packings, sheets, and the like.
• EBENB Metallocene EBT, produced by 100 parts by weight Mitsui Chemicals, Inc.
• HAF CB Asahi #70, produced by 50 parts by weight Asahi Carbon Co., Ltd.
• DBP oil absorption amount 101 ml/100 g; iodine value: 80 g/kg
• Zinc oxide 5 parts by weight Stearic acid 1 part by weight Fatty acid amide lubricant (Diamide O-200, 2 parts by weight produced by Nippon Kasei Chemical Company Limited; purified oleic acid amide) Plasticizer (Diana Process Oil PW-380, 5 parts by weight produced by Idemitsu Kosan Co., Ltd.);
• Antioxidant Irganox 1010, 1 part by weight produced by BASF Japan
• Organic peroxide Percumyl D, produced by 3 parts by weight NOF Corporation; dicumyl peroxide,
• Crosslinking accelerator Teaic, produced 0.5 parts by weight by Nippon Kasei Chemical Company Limited
• the components other than an organic peroxide and a crosslinking accelerator were each kneaded with a kneader. Then, the organic peroxide and the crosslinking accelerator were added and kneaded with an open roll.
• the obtained open roll kneaded material was evaluated for adhesion to the surface of the kneading machine and filler dispersibility. Further, the hardness of the crosslinked product was measured.
• the filler dispersibility evaluation was evaluated by a dispersion grader.
• Rubber hardness (JIS Duro A): according to JIS K6253-1: 2012 corresponding to ISO 18517
• a durometer hardness tester was used.
• Plate-like crosslinked rubber obtained by performing pressure vulcanization at 180° C. for 8 minutes and oven vulcanization (secondary vulcanization) at 180° C. for 24 hours was measured.
• Example 1 the same amount (50 parts by weight) of HAF-HS CB (Seast 3H, produced by Tokai Carbon Co., Ltd.; DBP oil absorption amount: 126 ml/100 g; iodine value: 84 g/kg) was used in place of the HAF CB.
• HAF-HS CB east 3H, produced by Tokai Carbon Co., Ltd.; DBP oil absorption amount: 126 ml/100 g; iodine value: 84 g/kg
• Example 1 the amount of the HAF CB was changed to 25 parts by weight, and 30 parts by weight of FEF CB (Asahi #60, produced by Asahi Carbon Co., Ltd.; DBP oil absorption amount: 114 ml/100 g; iodine value: 43 g/kg) was further used.
• FEF CB Asahi #60, produced by Asahi Carbon Co., Ltd.; DBP oil absorption amount: 114 ml/100 g; iodine value: 43 g/kg
• Example 1 the amount of the HAF CB was changed to 40 parts by weight, and 45 parts by weight of silica (Nipsil VN3, produced by Tosoh Silica Corporation) was further used.
• silica Niipsil VN3, produced by Tosoh Silica Corporation
• Example 1 the predetermined amount of another CB was used in place of the HAF CB.
• Table 2 below shows the evaluation and measurement results obtained in the above Examples and Comparative Examples.

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• Engineering & Computer Science (AREA)
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• Compositions Of Macromolecular Compounds (AREA)
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• 2019
  • 2019-03-14 JP JP2020509894A patent/JPWO2019188339A1/ja active Pending
  • 2019-03-14 CN CN201980017196.6A patent/CN111819238A/zh active Pending
  • 2019-03-14 WO PCT/JP2019/010522 patent/WO2019188339A1/fr unknown
  • 2019-03-14 US US16/982,329 patent/US20210009801A1/en not_active Abandoned
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